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at157l.txt Bull (1982) [27]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
mk9a.txt Denisov (1960) [31]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 12-120 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at198d.txt Desbordes (1993) [36]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at187a.txt Desbordes (1988) [34]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 2.5-18.2 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at187b.txt Desbordes (1988) [34]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 4.1-13.2 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at187c.txt Desbordes (1988) [34]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 4.1-45.6 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at187d.txt Desbordes (1988) [34]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 0.1-0.4 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at166b.txt Desbordes (1986) [37]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 4.1-12.2 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at197a.txt Desbordes (1993) [36]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 0.13-1 kPa Diluent: He Initial Temperature: 293 K Equivalence Ratio: 1
at197b.txt Desbordes (1993) [36]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 0.13-1 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at197c.txt Desbordes (1993) [36]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 0.13-1 kPa Diluent: Kr Initial Temperature: 293 K Equivalence Ratio: 1
at198a.txt Desbordes (1993) [36]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 0.13-1 kPa Diluent: He Initial Temperature: 293 K Equivalence Ratio: 1
at198b.txt Desbordes (1993) [36]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 0.13-1 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at198c.txt Desbordes (1993) [36]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 0.13-1 kPa Diluent: Kr Initial Temperature: 293 K Equivalence Ratio: 1
at166a.txt Edwards (1978) [41]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 2-9.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
js13c.txt Knystautas (1984) [52]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.4 - 3
mk7a.txt Knystautas (1982) [54]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at148a.txt Knystautas (1982) [54]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.3-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at150a.txt Knystautas (1982) [54]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 2-12 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 2.5
at150b.txt Knystautas (1982) [54]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 2-12 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 2.5
at151.txt Knystautas (1982) [54]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 2.7-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.625
at199c.txt Laberge (1993) [60]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.3-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at199d.txt Laberge (1993) [60]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.3-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 2.5
at86a.txt Lee (1982) [68]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at57f.txt Manzhalei (1974) [77]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 5.1-304 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at57c-mk.txt Manzhalei (1974) [77]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 4-614 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 2.5
mk157n.txt Moen (1984) [82]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: Air Initial Pressure: 92.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.5-0.61
mk6.txt Murray (1986) [89]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at184b.txt Pedley (1988) [95]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.3-13 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at129c.txt Strehlow (1969) [105]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.5-101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at129e.txt Strehlow (1969) [105]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.5-18.2 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.625
at129f.txt Strehlow (1969) [105]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 20.3-40.5 kPa Diluent: He Initial Temperature: 293 K Equivalence Ratio: 1
at69a.txt Strehlow (1967) [107]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 6.1-40.5 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at69b.txt Strehlow (1967) [107]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 6.1-40.5 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at172a.txt Tieszen (1991) [110]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: Air Initial Pressure: 101.325 kPa Diluent: Initial Temperature: 298-373 K Equivalence Ratio: 1
mk8b.txt Voitsekhovskii (1966) [121]
Category: cell size Fuel: C2H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 3.0-133 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
Edited Last: August 30, 1999